US2010282236A1PendingUtilityA1
Steam production
Est. expiryJul 25, 2027(~1 yrs left)· nominal 20-yr term from priority
C01B 5/00B01J 2219/1941B01J 2208/00212B01J 8/0278B01J 8/0285B01J 14/00B01J 4/002B01J 8/0221
42
PatentIndex Score
0
Cited by
0
References
0
Claims
Abstract
The present invention relates to an apparatus, in some embodiments a hand-held apparatus, and a method for the production of steam through contacting reactants and a catalyst.
Claims
exact text as granted — not AI-modified1 . An apparatus for the production of a product mixture comprising steam, said apparatus comprising a contacting means for bringing at least two liquid reactants into contact with a catalyst which catalyses an exothermic reaction between the at least two liquid reactants to produce the product mixture comprising steam.
2 . The apparatus according to claim 1 , wherein the contacting means comprises a reactant reservoir for containing the at least two liquid reactants and delivery means for delivering the aqueous solution to the catalyst.
3 . The apparatus according to claim 1 , wherein the contacting means comprises a first reactant reservoir for containing at least the first liquid reactant, a second reactant reservoir for containing at least the second liquid reactant and delivery means for delivering the liquid reactants to the catalyst.
4 . The apparatus according to claim 3 , wherein the first and second reactant reservoirs comprise separated compartments in a single body.
5 . The apparatus according to claim 1 , wherein the reactants comprise a peroxide and an organic compound.
6 . The apparatus according to claim 5 , wherein the peroxide is hydrogen peroxide.
7 . The apparatus according to claim 1 , wherein the reactants comprise an alcohol.
8 . The apparatus according to claim 7 , wherein the alcohol is methanol.
9 . The apparatus according to claim 8 , wherein the peroxide is hydrogen peroxide and wherein the molar ratio of hydrogen peroxide to methanol, when the liquid reactants contact the catalyst, is from about 10:1 to about 3:1.
10 . The apparatus according to claim 1 , wherein the delivery means is a means for passing the reactants across the catalyst.
11 . The apparatus according to claim 10 , wherein the delivery means comprises one or more pumps.
12 . The apparatus according to claim 11 , wherein at least one pump is a mechanical pump.
13 - 22 . (canceled)
23 . The apparatus according to claim 10 , wherein the means for passing the reactants across the catalyst causes the reactants to pass across the catalyst with a substantially even flow rate.
24 . The apparatus according to claim 23 , wherein a substantially even flow rate is an instantaneous flow rate which is within ±10% of the average flow rate.
25 - 26 . (canceled)
27 . The apparatus according to claim 1 , wherein the catalyst is of the formula x % Pt-y % Pd/[z % CZY-t % Al 2 O 3 —La 2 O 3 doped].
28 . The apparatus according to claim 1 , comprising a catalyst enclosure positioned around the catalyst.
29 - 33 . (canceled)
34 . The apparatus according to claim 1 , wherein the catalyst is in the form of a fixed bed reactor.
35 - 37 . (canceled)
38 . The apparatus a according to claim 34 , wherein the catalyst is in the form of a microchannel reactor.
39 - 53 . (canceled)
54 . A method of producing a product mixture comprising steam, comprising the step of bringing at least two liquid reactants into contact with a catalyst which catalyses an exothermic reaction between the at least two liquid reactants to produce the product mixture comprising steam, using the apparatus of claim 1 .
55 . A method of producing a product mixture comprising steam, comprising the step of bringing a solution containing at least two liquid reactants into contact with the catalyst which catalyses an exothermic reaction between the at least two liquid reactants to produce the product mixture comprising steam.
56 - 83 . (canceled)Cited by (0)
No later patents cite this yet.
References (0)
No backward citations on record.